chemical engineering process equipment and plant design Mcqs
4. High pressure fluid in a shell and tube heat exchanger should preferably be routed through the________________?
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A. Shell side for smaller total pressure drop

B. Shell side for large overall heat transfer co-efficient

C. Shell side, if the flow is counter-current and tube side if the flow is co-current

D. Tubes to avoid the expansion of high pressure shell construction
5. The LMTD correction factor (FT) is defined as the __________________?
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A. Ratio of LMTD to the true temperature difference

B. Ratio of true temperature difference to the LMTD

C. Geometric mean of the true temperature difference and the LMTD

D. Differenced of true temperature difference and the LMTD

9. Value of Peclet number = 0, is the representative of ____________________?
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A. Plug flow

B. Complete back mixing

C. Eddy diffusivity = 0

D. Laminar flow

10. The minimum baffle height should be ______________?
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A. Twice the impeller diameter

B. 3/4 of the tank height

C. Twice the tank diameter

D. Equal to the impeller diameter

14. For a cylindrical shell, (subject to the thickness of uppermost course being more than the minimum for dia of the tank in question), the thickness of the courses of shell_________________?
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A. ld be maintained inside the shell

B. May decrease or increase upwards depending upon whether vacuum or positive pressure

C. Decreases upwards

D. Remains same throughout

E. Increases upwards

15. In a shell and tube heat exchanger, the shortest centre to centre distance between the adjacent tubes is__________________?
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A. Called tube pitch

B. Always less than the diameter of the tube

C. Called tube clearance

D. None of these

16. Power required for agitation depends upon the______________________?
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A. Agitator type & speed of agitation

B. Height & properties of the liquid

C. Size of agitator & the tank

D. All A., B. and C.
21. Baffle spacing is generally _________________ the I.D. of the shell ?
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A. More than

B. Not greater than

C. Not less than one fifth of

D. Both B. and C.
25. The dust collection efficiency of a cyclone separator_________________?
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A. None of these

B. Decreases with increase in gas flow rate

C. Is inversely proportional to the mass of the dust particle

D. Is directly proportional to the radius of the dust particle path

27. Bubble cap tray is the most commonly used tray in large distillation column, because______________?
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A. It incurs less pressure drop as compared to any other try designed for the same duty

B. It eliminates the foaming and entrainment tendency during operation

C. None of these

D. Of its flexibility and nearly constant efficiency under varying conditions of operation
28. 1.2 to 3.8 cms is the value of the ______________________?
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A. All A., B. and C.

B. Skirt clearance for bubble caps

C. Downcomer liquid seal in case of a balanced tray design

D. Static submergence in case of a bubble cap tray for column operating under pressure (? 1 atm)

30. Pick out the wrong statement?
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A. The discharge end of the downcomer must project far enough into the tray liquid so that no

B. If sufficient residence time (around 8 seconds) is not provided to the downcoming liquid in

C. None of these

D. The liquid head in the downcomer should not be greater than one half the plate spacing to

E. downcomer, it may entrain some vapour

F. id flooding

32. The length of straight rectangular weir used on cross-flow trays is generally ________________ the column diameter ?
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A. 2 ft irrespective of (for column > 3 ft diameter)

B. Twice

C. Equal to

D. 0.6-0.8 times
34. In a shell and tube heat exchanger, the clearance of the tube is generally___________________?
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A. Not less than one-fourth of the tube diameter or 3/16?

B. More than the tube diameter

C. Equal to the tube diameter

D. More in case of triangular pitch as compared to the square pitch tube layout

40. Pick out the wrong statement pertaining to shell and tube heat exchanger_______________?
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A. Tie rods are fixed at one end in the tube sheet by making blind holes and the minimum

B. Clearance between shell & baffles and between tube & baffles should be minimum to avoid

C. Baffles are supported independently of the tubes by tie rods and positioned by spacers

D. Bracket supports are used for horizontal shell, while saddle support is used for vertical shell

E. ber of tie rods is 4 with at least 10 mm diameter

F. passing of the fluid, but it should be enough to permit the removal of tube bundle

42. Pick out the wrong statement pertaining to the design of a horizontal tube evaporator ?
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A. Its usual dimensions are: tube dia = 2-3 cms; evaporator body dia = 1-4 metres and evaporator

B. Liquor flows inside the tube, while the steam is outside submerging the tube

C. It is suitable for process, in which the final product is a liquor instead of solid

D. ght = 2.5-4 metres

E. It is unsuitable for concentrating those liquids, which form a scale or deposit salt

43. ______________ closure is the weakest enclosure for cylindrical vessels?
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A. Elliptical

B. Hemispherical

C. Torispherical

D. Conical or flat plate
46. Wind load consideration in the design of a support can be neglected, when the vessel is___________________?
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A. Tall but empty

B. Tall (say 30 metres), but is full of liquid

C. Short (< 2 m) and housed indoor

D. None of these

47. The necessary wall thickness for a metallic storage vessel is a function of the ___________________?
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A. Diameter of the vessel

B. All A., B. and C.

C. Ultimate tensile strength (or yield point) of the material and operating temperature

D. Operating pressure and welding/joint efficiency

48. In a double pipe (concentric) heat exchanger, the hydraulic radius for heat transfer (for a fluid flowing through the annulus) would be_________________?
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A. Less than that for fluid flow

B. Same as that for fluid flow

C. More than that for fluid flow

D. D2 D1 (D1 and D2 are I.D. of inner and outer pipes respectively)